Scientific Journal of Frontier Chemical Development June 2013, Volume 3, Issue 2, PP.25-29
Copper-Catalyzed Allylic Oxidation of Cyclohexene with Molecular Oxygen Xu Zhang 1, Rong Yi 1, Tian Chen 1, Shichun Ni 2, Genlin Wang 2, Lei Yu #, 1, 2 1. School of Chemistry and Chemical Engineering, Yangzhou University, Yangzhou, 225002，People’s Republic of China 2. Jiangsu Yangnong Chemical Group Co. Ltd., Yangzhou, 225009, People’s Republic of China #Email: yulei@yzu.edu.cn
Abstract Copper-catalyzed aerobic allylic oxidation of cyclohexene under solvent-free conditions leads to 2-cyclohexenol and 2cyclohexenone, the important intermediates in chemurgy. This pathway is suitable for industrial production, owing to the high conversion rate and selectivity, the solvent-free conditions, the cheap catalyst and the environment-friendly oxidant and procedure. Keywords: Catalysis; Copper; Allylic Oxidation; Aerobic Oxidation; Cyclohexene.
1 INTRODUCTION The allylic oxidation of olefins is one of the most important topics in both academic and industrial researches. In this process, olefins are converted to unsaturated alcohols or ketones while the C=C bond is preserved.1 The allylic oxidation of cyclohexene is a typical example, since the products 2-cyclohexenol and 2-cyclohexenone are very useful compounds in chemurgy.2 Up to the present, the catalytic allylic oxidation of cyclohexene has drawn much attention and many effective catalysts have been developed, such as metal nanoparticles,3-5(Table 1, entries 1-3) metal–organic frameworks,6(Table 1, entry 4) metal porphyrin complexes 7-9(Table 1, entries 5-7) and non-metal catalysts.10(Table 1, entry 8) However, some of the above catalysts have resulted in low conversion rates and low selectivity, 6 on the other hand, many of them require organic solvents 3-5, 7-10, 12 and chemical oxidants.3 Recently, gold has also been found to have strong catalic ability in the allylic oxidation of cyclohexene. 11-13(Table 1, entries 911) However, the high price hinders their large scale applications. The ideal catalytic oxidation process suitable for industrial production expected to employ molecular oxygen as the oxidant, simple and abundant catalyst, is carried out in solvent-free conditions.14 Our group has been trying to achieve this goal in cyclohexene’s oxidation for a long time. Recently, the transition metal-catalyzed allylic oxidation of cyclohexene has been investigated by molecular oxygen and it was found that catalyzed by copper, the oxidation of cyclohexene by molecular oxygen led to 2cyclohexenol and 2-cyclohexenone with high conversion rate and selectivity in solvent-free conditions.(Table 1, entry 12) Herein, our findings were available. TABLE 1 THE ALLYLIC OXIDATION OF CYCLOHEXENE REPORTED BY RECENT LITERATURES.
OH [O] cat. 1 Entry 1 2 3 4 5 6 7
Catalyst CuO CoO CoHAP-γ-Fe2O3 Cu/Co-MOFs Fe-Por Mn-Por Ru-Por
O +
2 Oxidant TBHP O2 H2O2 O2 O2 O2 O2
Solvent CH3CN c-C6H12 MeCN MeOH/MeCN MeCN MeCN - 25 www.sjfcd.org
3 Conv. (%) 99 97 88 33 100 72 100
2+ 3 Select. (%) 95 80 81 44 99 67 94
Ref. 3 4 5 6 7 8 9
TABLE 1 THE ALLYLIC OXIDATION OF CYCLOHEXENE REPORTED BY RECENT LITERATURES (CONTINUE)
Entry 8 9 10 11 12
Catalyst NHPA + DADCAQ Au/SiO2 Au/SBA-15-Py Au/La-OMS-2 Cu(OAc)2.H2O
Oxidant O2 H2O2 O2 O2 O2
Solvent DMACa toluene -
Conv. (%) 84 68 54 48 66
2+ 3 Select. (%) 69 80 57 84 79
Ref. 10 11 12 13 This work
a N,N’-dimethylacetamide
2 RESULTS AND DISCUSSION We initially examined the oxidation of cyclohexene in 1,4-dioxane catalyzed by Cu(CF3CO2)2- MnO2 bi-catalysts (Table 2, entry 1). After the mixture was stirred at 80oC in air for 24 hours, the GC analysis indicated that 63% of cyclohexene was converted and both cyclohexenol 2 and cyclohexenone 3 were generated with 11% and 31% selectivity respectively. Further investigations showed that phosphorus ligand would restrain the reaction (Table 2, entry 2) and both Cu(CF3CO2)2 and MnO2 could catalyze the reaction independently (Table 2, entries 3-4). The screenings (Table 2, entries 5-11) demonstrated that Cu(OAc)2H2O was the better catalyst and the conversion rate of cyclohexene could reach 79 % with higher selectivity (Table 2, entry 8). TABLE 2 SCREENING OF CATALYSTS IN 1,4-DIOXANE.a
+
1,4-dioxane, air, 80oC, 24h 1
entry 1 2 3 4 5 6 7 8 9 10 11 a1
Catalyst (amount/mol%) Cu(CF3CO2)2 (3), MnO2 (9) Cu(CF3CO2)2 (3), MnO2 (9), PPh3 (12) MnO2 (9) Cu(CF3CO2)2 (3) Cu(NO3)2 (3) CuBr2 (3) CuCl2 (3) Cu(OAc)2H2O (3) Mn(OAc)3(3) Ce(NH4)2(NO3)6(3) CuO (3)
O
OH
catalyst 3 mol%
2
3
Conv. (%) 63
Select. of 2 (%) 11
Select. of 3 (%) 31
Select. of 2+3 (%) 42
2
0
0
0
9 77 60 19 64 79 10 64 67
12 8 13 27 11 7 28 2 14
50 21 50 26 56 61 72 49 32
62 29 63 53 67 68 100 51 46
mmol cyclohexene and 2 mL solvent was used; the catalyst amount was based on cyclohexene; The results were detected by GC.
Then, effects of solvents were examined and the reactions were taken in different solvents, such as 1, 4-dioxane, cyclohexane, EtOAc and so on (Table 3, entries 1-7). In terms of the balance of conversion and selectivity, 1, 4dioxane was the better solvent (Table 3, entry 1). Although the selectivity of 2 and 3 was higher in cyclohexane, the conversion of cyclohexene was very low (Table 3, entry 2). Contrastively, the reaction in CH3CN had the higher conversion of cyclohexene but the slightly lower selectivity of 2 and 3 (Table 3, entry 5). To enhance the conversion rate of cyclohexene in 1, 4-dioxane, pure O2 was employed. Although this condition afforded a full conversion of cyclohexene, the selectivity decreased obviously and 1, 2-ethanedioldiformate, an oxydate of solvent, was also observed from GC-MZ (Table 3, entry 8; Scheme 1). Inspired by this result, we carried out the reaction in solventfree conditions and the total selectivity was roughly satisfied (Table 3, entry 9). TABLE 3 SCREENING OF SOLVENTS.a
Cu(OAc)2H2O 3 mol%
+
solvent, air, 80oC, 24h 1
2 - 26 www.sjfcd.org
O
OH
3
Entry 1 2 3 4 5 6 7 8 9 a
solvent 1,4-dioxane cyclohexane EtOAcb DMSO CH3CN DMF Benzeneb 1,4-dioxanec -c, d
Conversion (%) 79 26 58 82 94 38 44 100 41
Select. of 2 (%) 7 31 13 23 18 35 24 3 28
Select. of 3 (%) 61 49 24 35 49 39 28 46 50
Select. of 2+3 (%) 68 80 37 58 67 74 52 49 78
1 mmol cyclohexene, 3 mol % catalyst and 2 mL solvent was used. The results were detected by GC. b Reflux. c Pure O2 and
d
9.5
mmol of cyclohexene were employed.
[O]
O
OHC
O
O
CHO
O 1,2-ethanedioldiformate SCHEME 1 THE OXIDATION OF 1, 4-DIOXANE.
In industrial production, the reactions in solvent-free conditions could afford higher capacity than those taken in solvents. Therefore, although the conversion rate was lower, the result in table 3, entry 9, would be more effective than any other reactions taken in solvents. In order to gain more improved reaction conditions, further conditional screenings were taken (Table 4). Results in table 4, entries 1-5 showed that the conversion rate of cyclohexene was restrained at high temperature. However, the temperature did not significantly affect the total selectivity of 2 and 3. By comparison of the results in table 4, entries 2, 6 and 7, it was obvious that the reaction time greatly affected the conversion of cyclohexene. The best conditions in table 4 should be the results in entry 2. To examine its reliability in larger scale preparation, the reaction under this condition was also taken in a 10 time larger scale in a 1 L flask charged with O2 and the product was separated by distillation. Cyclohexene was recovered in 34 % yield (66% conversion rate) while a 2/3 mixture was obtained in 52% yield (79% total selectivity). TABLE 4 OXIDATION OF CYCLOHEXENE IN A SEALED TUBE WITHOUT SOLVENT.A
Cu(OAc)2H2O 3 mol%
+
neat, O2 1 entry 1 2 3 4 5 6 7 a
t/oC 40 60 80 100 120 60 60
t/h 24 24 24 24 24 6 16
2 Conv. (%) 56 61 41 24 17 39 46
Select. of 2 (%) 34 30 28 33 32 28 32
O
OH
3 Select. of 3 (%) 39 47 50 44 43 45 46
Select. of 2+3 (%) 73 77 78 77 75 73 78
9.5 mmol of cyclohexene and 3 mol% of Cu(OAc)2.H2O were heated in a 100 mL sealed tube charged with O2; The results were
detected by GC.
Based on the literatures 5-21 as well as our previous investigations, 22-23 it was proposed that the reaction underwent through a single-electron-transfer (SET) triggered by free radical mechanism. The SET reaction of Cu (II) [19] with cyclohexene 1 afforded the intermediate 4 and initiated the free radical chain (Scheme 2, eq. 1). The oxidation of 4 with O2 led to the peroxide free radical 5 (Scheme 2, eq. 2), which seized hydrogen from 1 to generate the 3hydroperoxy-1-cyclohexene 6 and regenerate the free radical 4. The dehydration of 6 gave the product cyclohexenone 3 (Scheme 2, eq. 3). There are two possible pathways in the chain termination step: (1) the dimerizations of free radical 4 lead to the by-product 7 (Scheme 2, eq. 4; This by-product was observed in GC-MZ analysis, further proving the mechanisms we supposed); (2) the hydrogen capture from water lead to the starting material 1 and hydroxyl free radical, which reacted with the free radical 4 to give another product 2 (Scheme 2. eq. 5 and 6). - 27 www.sjfcd.org
Cu(I), H+
Cu(II)
(1) 1
Chain initiation
4 O
O
O2 (2) 4
O
O
5 4
1
H O
Chain conduction O
O
(3) 5
H2O
6
+
3
(4)
4
4
7 Chain termination
+ H2O
+ HO
(5)
1
4
OH HO
+
(6) 4
2
SCHEME 2 PROPOSED MECHANISMS.
3 CONCLUSIONS In conclusion, copper-catalyzed oxidation of cyclohexene with molecular oxygen afforded the mixture of 2cyclohexenol and 2-cyclohexenone. In industrial production, the catalyzed dehydrogenation of 2-cyclohexenol easily led to 2-cyclohexenone, useful intermediates in herbicide production. Therefore, this reaction is potentially useful in the production of 2-cyclohexenone. Compared with literatures, our method has the following advantages: (1) The cheap catalyst; (2) The abundant and clean oxidant; (3) The highly atom economic procedure; (4) The solvent-free conditions and the satisfied product selectivity. Our group is now trying to apply this method in larger scale preparation.
ACKNOWLEDGMENT We thank NNSFC (21202141), Priority Academic Program Development of Jiangsu Higher Education Institutions, and the opening foundation of the Key Laboratory of Environmental Materials and Engineering of Jiangsu Province (K11024, K090030) for financial support as well as the Analysis Centre of Yangzhou University.
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AUTHORS Lei Yu. Born in July 1982, Ph. D.
Rong Yi. Master student. Research direction: Organic Synthesis;
Associate
Professor
Email: juran1987@126.com.
University;
P.
I.
of of
Yangzhou the
Organic
Methodology Group, School of Chemistry & Chemical Engineering; Head of the
Tian Chen. Associate Professor. Research direction: Organic Synthesis; Email: chen_t_yz@163.com.
Graduate Work Station, Jiangsu Yangnong
Shichun Ni.Worker. Research direction: Chemurgy.
Chemical Group Co. Ltd.
Genlin Wang. Research Group Leader. Research direction:
Xu Zhang. Ph. D. Research direction: Organic Synthesis;
Chemurgy; Email: genlinwang@163.com.
Email: zhangxu@yzu.edu.cn.
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